the coking properties of coal at elevated pressures. - Argonne ...
the coking properties of coal at elevated pressures. - Argonne ...
the coking properties of coal at elevated pressures. - Argonne ...
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under which conditions sulfur species gener<strong>at</strong>ed during <strong>the</strong> combustion <strong>of</strong> pulverized<br />
<strong>coal</strong> can be captured and retained by calcium containing sorbents. Two series <strong>of</strong><br />
experiments were carried out: one in which any capture would take place primarily<br />
under oxidizing conditions and <strong>the</strong> o<strong>the</strong>r in which significant residence times in<br />
<strong>the</strong> rich zone would allow capture under reducing conditions. Under oxidizing conditions<br />
<strong>the</strong> <strong>the</strong>rmal environment experienced by <strong>the</strong> sorbent particle appears to be <strong>the</strong><br />
dominant parameter controlling sulfur capture. This is probably because <strong>of</strong> deadburning.<br />
If a sorbent particle's temper<strong>at</strong>ure exceeds a certain limit (which depends<br />
on <strong>the</strong> particular sorbent) <strong>the</strong> sorbent deadburns and loses its reactivity (4).<br />
The processes controlling capture and retention when <strong>the</strong> sorbent is maintained<br />
under reducing conditions for a prolonged time are more complex. The principle<br />
gas phase sulfur specie are HzS, SO2 and COS and, even though <strong>the</strong> sulfur species are<br />
absorbed <strong>the</strong> possibility th<strong>at</strong> <strong>the</strong> sulfide will decompose during burnout exists.<br />
The d<strong>at</strong>a presented in Figure 6 shows a significant difference between <strong>the</strong> behavior<br />
<strong>of</strong> <strong>coal</strong> and propane doped with H2S. This difference can be <strong>at</strong>tributed to:<br />
- With <strong>coal</strong> part <strong>of</strong> <strong>the</strong> fuel remains in <strong>the</strong> solid phase and for a given<br />
input stoichiometry <strong>the</strong> gas phase stoichiometry in <strong>the</strong> reducing zone is<br />
higher than with gas. Reference to Figure 1 indic<strong>at</strong>es th<strong>at</strong> <strong>the</strong> stability<br />
<strong>of</strong> calcium sulfide is strongly dependent upon stoichiometry r<strong>at</strong>io;<br />
-<br />
With <strong>coal</strong> up to 50 percent <strong>of</strong> <strong>the</strong> sulfur remains in <strong>the</strong> solid phase under<br />
rich conditions thus <strong>the</strong> gas phase concentr<strong>at</strong>ion is lower than <strong>the</strong> corres-<br />
ponding concentr<strong>at</strong>ion with propane as <strong>the</strong> fuel;<br />
- The conditions during burnout in <strong>the</strong> second stage will be different for <strong>the</strong><br />
solid and gaseous fuels and this could affect retention <strong>of</strong> <strong>the</strong> sulfur<br />
during burnout.<br />
These tests indic<strong>at</strong>e th<strong>at</strong> <strong>the</strong>re is <strong>the</strong> potential to remove gre<strong>at</strong>er than 50<br />
percent <strong>of</strong> <strong>the</strong> input sulfur with Ca/S molar r<strong>at</strong>ios <strong>of</strong> two when <strong>coal</strong> is burned<br />
under low NOx conditions. Fur<strong>the</strong>r work is necessary to insure th<strong>at</strong> <strong>the</strong> controlling<br />
conditions can be achieved in practical combustors and th<strong>at</strong> <strong>the</strong> sorbent injection<br />
does not adversely impact combustor performance.<br />
References<br />
1.<br />
2.<br />
3.<br />
4.<br />
5.<br />
6.<br />
Gartrell, F.F., "Full Scale Desulfuriz<strong>at</strong>ion <strong>of</strong> Stack Gas by Dry Limestone<br />
Injection", EPA-650/2-73-019 a, b, c, 1973.<br />
Zallen, D.M., Gershman, R., Heap, M.P., Nurick, W.H., "The Generaliz<strong>at</strong>ion <strong>of</strong><br />
Low Emission Coal Burner Technology", Proceedings, Third St<strong>at</strong>ionary Source<br />
Combustion Symposium, EPA-600/7-70-050 b, 1979.<br />
Flament, G., "The Simultaneous Reduction <strong>of</strong> NOx and SO2 in Coal Flames by<br />
Direct Injection <strong>of</strong> Sorbents in a Staged Mixing Burner", IFRF doc. no.<br />
G 19/a/10, 1981.<br />
Coutant, R.W., et al., "Investig<strong>at</strong>ion <strong>of</strong> <strong>the</strong> Reactivity <strong>of</strong> Limestone and<br />
Dolomite for Capturing SO2 from Flue Gas", B<strong>at</strong>elle Memorial Institute,<br />
Final Report, EPA Contract PH-86-67-115, 1970.<br />
Borgwardt, R.H., "Kinetic <strong>of</strong> <strong>the</strong> Reaction <strong>of</strong> SO2 with Calcined Limestone",<br />
NAPCA, Vol. 4, p. 59, 1970.<br />
Borgwardt, R.H., Present<strong>at</strong>ion <strong>at</strong> <strong>the</strong> EPA SPO Contractors Meeting, Raleigh,<br />
North Carolina, October 1981.<br />
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